EP0395604B1 - Centrifugal pump - Google Patents

Centrifugal pump Download PDF

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Publication number
EP0395604B1
EP0395604B1 EP90850102A EP90850102A EP0395604B1 EP 0395604 B1 EP0395604 B1 EP 0395604B1 EP 90850102 A EP90850102 A EP 90850102A EP 90850102 A EP90850102 A EP 90850102A EP 0395604 B1 EP0395604 B1 EP 0395604B1
Authority
EP
European Patent Office
Prior art keywords
impeller
insert part
centrifugal pump
cutting means
pump
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP90850102A
Other languages
German (de)
French (fr)
Other versions
EP0395604A1 (en
Inventor
Bengt Södergard
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xylem Water Solutions AB
Original Assignee
ITT Flygt AB
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ITT Flygt AB filed Critical ITT Flygt AB
Publication of EP0395604A1 publication Critical patent/EP0395604A1/en
Application granted granted Critical
Publication of EP0395604B1 publication Critical patent/EP0395604B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D7/00—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts
    • F04D7/02—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type
    • F04D7/04—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type the fluids being viscous or non-homogenous
    • F04D7/045—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type the fluids being viscous or non-homogenous with means for comminuting, mixing stirring or otherwise treating
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00—Details, component parts, or accessories
    • F04D29/18—Rotors
    • F04D29/22—Rotors specially for centrifugal pumps
    • F04D29/2261—Rotors specially for centrifugal pumps with special measures
    • F04D29/2288—Rotors specially for centrifugal pumps with special measures for comminuting, mixing or separating

Definitions

  • This invention concerns a centrifugal pump for pumping liquids containing solid bodies, such as rags and other elongated objects.
  • the centrifugal pump which sucks the liquid into its center and throws it outwards in the direction of the periphery, has good qualities when pumping clean liquids.
  • the liquid contains solid bodies, however, the problem arises that these may got stuck between the pump impeller and the surrounding pump housing and cause a stop or at least a decreased pumping ability.
  • a way to solve these problems is to design the pump in such a way that the impeller rotates beside the flow itself, so-called vortex impellers.
  • vortex impellers By this the clogging problems may be essentially solved, however, at the cost of other disadvantages, such as a decreased efficiency.
  • the front end of the impeller is provided with two cutting means which cooperate with the inlet of the impeller for cutting the pollutions. It turns out, however, that the under pressure in the pump inlet makes an incoming rag to get sucked into the center of the impeller. Smaller rags may then rotate together with the impeller without making contact with the cutting means. Bigger rags may cause an increasing rotary resistance, sometimes to such a degree that the pump stops.
  • the two described impellers have in common that they are both of the so-called open type. This means that the impeller has got only one cover disc on which the vanes are mounted and that the impeller is open towards the cutting means. This embodiment depends on the fact that the prevailing opinion has been that only open impellers are possible to use when pumping strongly polluted liquids.
  • the closed impeller which is provided with two cover discs and vanes therebetween, has above all the advantage that its efficiency is far better than that of an open impeller.
  • US-A-1551 918 shows a complicated device where a closed impeller is used and which includes two cutting devices and an intermediate room where rags etc are bound to clog.
  • Fig 1 shows a section view of a submersible pump provided with a device according to the invention, while Fig 2 shows the device in more detail.
  • Fig 3 and 4 show two sections of the impeller.
  • FIG. 1 stands for a pump with a pump housing 2 having an inlet opening 3 with an insert part 4 provided with grooves 5.
  • 6 stands for a centrifugal impeller with inlet, hub 7, primary cutting means 8, secondary cutting means 9 and projections 10.
  • 11 and 12 stand for the upper and lower cover discs respectively of the impeller 6.
  • 13 stands for vanes, while 14 and 15 stand for collars on the lower cover disc 12.
  • the pump impeller 6 is thus designed with a cylinder-formed hub 7, which extends downwards into the inlet opening of the pump housing 2.
  • a number of cutting means 8, 9 are arranged on the inlet 3, which cooperate with axially directed grooves 5 in the inlet opening to cut pollutions in the water to be pumped.
  • the impeller is further designed with two cover discs 11 and 12 and intermediate vanes 13.
  • the cover disc 12 is provided with a collar 14, which surrounds the upper end of the insert part 4, thus obtaining a radial seal.
  • This seal which may have a length of between 3 and 6 mm, prevents effectively material from entering along the underside of the cover disc 12 and cause clogging.
  • a similar radial seal is created between the collar 14 and the part of the pump housing 2, which is situated radially outside said collar.
  • the lower cover disc 12 is provided with a collar 15, which extends a distance inwards over the insert part 4, thus creating an axial seal which additionally decreases the risk for the cut material being fed below the cover disc 12.
  • a pump is obtained which has very good qualities when pumping strongly polluted liquids.
  • the closed impeller has a far better efficiency.
  • the risks for clogging and over-load of the driving motor are considerably reduced as all material is cut close to the center of the impeller. This means shorter lever arms for the forces and thus less torque.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Iron Core Of Rotating Electric Machines (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Saccharide Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Lubricants (AREA)

Abstract

The invention concerns a centrifugal pump for pumping polluted liquids. The pump comprises an impeller (6) of a so-called closed type having two cover discs (11) and (12) respectively and vanes (13) therebetween. The inner parts of the vanes (13) cooperate with cutting means (5) within the pump inlet, while the lower cover disc (12) together with a non-rotating insert part (4) in the pump inlet create a radial seal, which prevents medium from entering beside of the impeller (6).

Description

  • This invention concerns a centrifugal pump for pumping liquids containing solid bodies, such as rags and other elongated objects.
  • The centrifugal pump, which sucks the liquid into its center and throws it outwards in the direction of the periphery, has good qualities when pumping clean liquids. When the liquid contains solid bodies, however, the problem arises that these may got stuck between the pump impeller and the surrounding pump housing and cause a stop or at least a decreased pumping ability.
  • A way to solve these problems is to design the pump in such a way that the impeller rotates beside the flow itself, so-called vortex impellers. By this the clogging problems may be essentially solved, however, at the cost of other disadvantages, such as a decreased efficiency.
  • Another way to solve the problems, is to arrange some form of cutting means in front of the impeller which cuts rags and the like and makes them possible to pump. An example of such a solution is shown in the US Pat No 4 108 386.
  • In the known construction the front end of the impeller is provided with two cutting means which cooperate with the inlet of the impeller for cutting the pollutions. It turns out, however, that the under pressure in the pump inlet makes an incoming rag to get sucked into the center of the impeller. Smaller rags may then rotate together with the impeller without making contact with the cutting means. Bigger rags may cause an increasing rotary resistance, sometimes to such a degree that the pump stops.
  • Another construction is shown in the Swedish published patent application No 444 969. Here a central body with cutting means is arranged, which body fills up the space in the inlet, thus diminishing the risk for the rags being sucked into the impeller center. This solution is normally working very well, but under certain conditions a rag may stick to the center of the impeller and get stretched outwards to the periphery between the impeller and the housing. The friction which derives from that might lead to an overload of the motor and release of the motor protection device.
  • The two described impellers have in common that they are both of the so-called open type. This means that the impeller has got only one cover disc on which the vanes are mounted and that the impeller is open towards the cutting means. This embodiment depends on the fact that the prevailing opinion has been that only open impellers are possible to use when pumping strongly polluted liquids.
  • The closed impeller, which is provided with two cover discs and vanes therebetween, has above all the advantage that its efficiency is far better than that of an open impeller.
  • US-A-1551 918, shows a complicated device where a closed impeller is used and which includes two cutting devices and an intermediate room where rags etc are bound to clog.
  • According to the invention, use of a closed impeller when pumping strongly polluted liquids has been made possible. This possibility brings about better efficiency and a longer bearing life time. In addition it gives a better cutting result, thus diminishing the risks for clogging and damage.
  • The invention is more closely described below with reference to the enclosed drawings.
  • Fig 1 shows a section view of a submersible pump provided with a device according to the invention, while Fig 2 shows the device in more detail. Fig 3 and 4 show two sections of the impeller.
  • In the drawings 1 stands for a pump with a pump housing 2 having an inlet opening 3 with an insert part 4 provided with grooves 5. 6 stands for a centrifugal impeller with inlet, hub 7, primary cutting means 8, secondary cutting means 9 and projections 10. 11 and 12 stand for the upper and lower cover discs respectively of the impeller 6. 13 stands for vanes, while 14 and 15 stand for collars on the lower cover disc 12.
  • The pump impeller 6 is thus designed with a cylinder-formed hub 7, which extends downwards into the inlet opening of the pump housing 2. A number of cutting means 8, 9 are arranged on the inlet 3, which cooperate with axially directed grooves 5 in the inlet opening to cut pollutions in the water to be pumped.
  • The impeller is further designed with two cover discs 11 and 12 and intermediate vanes 13. The cover disc 12, which is heading the pump inlet 3, stops a certain distance from the hub 7 thus creating a ringformed opening around the hub, through which opening the pumped medium is sucked into the impeller.
  • Pollutions in the liquid shall, as previously mentioned, be cut between the cutting means 8, 9 and the grooves 5. The vanes 13 and the insert part 4 provided with the grooves 5 with its end surface create together another cutting means which effectively mills the pollutions. When mounting, the insert part 4 is brought into contact with the inner parts of the vanes 13, which gives a suitable cutting distance, when the impeller starts rotating. An additional advantage with the invention is thus that a correct distance between impeller and insert part is easily and automatically obtained.
  • In order to secure that the entire amount of cut material is brought into the impeller through the ring-formed opening, the cover disc 12 is provided with a collar 14, which surrounds the upper end of the insert part 4, thus obtaining a radial seal. This seal, which may have a length of between 3 and 6 mm, prevents effectively material from entering along the underside of the cover disc 12 and cause clogging. A similar radial seal is created between the collar 14 and the part of the pump housing 2, which is situated radially outside said collar.
  • According to a special embodiment the lower cover disc 12 is provided with a collar 15, which extends a distance inwards over the insert part 4, thus creating an axial seal which additionally decreases the risk for the cut material being fed below the cover disc 12.
  • By help of the invention a pump is obtained which has very good qualities when pumping strongly polluted liquids. As compared with previously used open impellers, the closed impeller has a far better efficiency. In addition the risks for clogging and over-load of the driving motor are considerably reduced as all material is cut close to the center of the impeller. This means shorter lever arms for the forces and thus less torque. Finally there is no risk for collection of braking material between the impeller and the bottom of the pump housing.

Claims (4)

  1. A centrifugal pump for pumping liquids containing solid bodies and pollutions such as rags and other elongated objects and comprising a pump housing (2) having a central inlet (3) and a rotating impeller (6) designed as a closed impeller having upper and lower cover discs (11) and (12) respectively and intermediate vanes (13) and being provided with cutting means (8,9) which cooperate with an insert part within the pump inlet (3) which insert part is provided with grooves (5) which obtain a cutting between the cutting means and the edges of the grooves, characterized in that the lower cover disc (12) is provided with a collar (14) which surrounds the end of the insert part (4) heading the impeller (6) thus creating a radial seal.
  2. A centrifugal pump according to claim 1, characterized in that the collar (14) together with the part of the pump housing (2) radially surrounding said collar also creates a radial seal.
  3. A centrifugal pump according to claim 1, characterized in that the lower cover disc (12) is provided with a collar (15) which extends a distance inwards over the insert part (4), thus creating an axial seal between those parts.
  4. A centrifugal pump according to claim 1, characterized in that parts of the vanes (13), which are close to the hub (7) of the impeller (6) create cutting means in cooperation with the end of the insert part (4) heading the impeller (6).
EP90850102A 1989-04-27 1990-03-09 Centrifugal pump Expired - Lifetime EP0395604B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8901534A SE466766B (en) 1989-04-27 1989-04-27 Centrifugal pump intended for pumping of liquids containing solid particles, for example, rags and other long-stretched objects
SE8901534 1989-04-27

Publications (2)

Publication Number Publication Date
EP0395604A1 EP0395604A1 (en) 1990-10-31
EP0395604B1 true EP0395604B1 (en) 1993-12-22

Family

ID=20375817

Family Applications (1)

Application Number Title Priority Date Filing Date
EP90850102A Expired - Lifetime EP0395604B1 (en) 1989-04-27 1990-03-09 Centrifugal pump

Country Status (11)

Country Link
US (1) US5011370A (en)
EP (1) EP0395604B1 (en)
JP (1) JPH07111191B2 (en)
AT (1) ATE99025T1 (en)
AU (1) AU622763B2 (en)
CA (1) CA2015572C (en)
DE (1) DE69005351T2 (en)
DK (1) DK0395604T3 (en)
FI (1) FI101824B (en)
NO (1) NO172308C (en)
SE (1) SE466766B (en)

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4128281A1 (en) * 1991-08-27 1993-03-04 Abs Pumpen Ag Pump for handling domestic sewage - has disc with cutting blades arranged in front of pump inlet
DE4338931C2 (en) * 1993-11-15 1996-09-05 Wilo Gmbh Non-clogging centrifugal pump
DE4438841C2 (en) * 1994-11-02 1999-05-27 Orpu Gmbh Pump with a cutting device
CH689058A5 (en) * 1994-11-28 1998-08-31 Haeny & Cie Ag Centrifugal pump for contaminated with solids sewage waters.
SE520417C2 (en) * 1997-12-18 2003-07-08 Flygt Ab Itt Pump of centrifugal or semi-axial type intended for pumping of uncontaminated wastewater
US6089823A (en) * 1998-05-04 2000-07-18 Ingersoll-Dresser Pump Company Multi-stage vertical turbine pump with comminution
SE520740C2 (en) * 1998-06-30 2003-08-19 Abs Pump Prod Ab centrifugal
DE20114891U1 (en) * 2001-09-10 2001-11-15 Grundfos As Sewage centrifugal pump
SE524048C2 (en) * 2002-04-26 2004-06-22 Itt Mfg Enterprises Inc Device at pump
SE525412C2 (en) 2003-10-20 2005-02-15 Itt Mfg Enterprises Inc Centrifugal pump for contaminated liquids, comprises wheel with scoops and cover plates with spiral grooves around casing inlet
US7037069B2 (en) * 2003-10-31 2006-05-02 The Gorman-Rupp Co. Impeller and wear plate
SE0402840L (en) * 2004-11-19 2006-04-11 Itt Mfg Enterprises Inc Impeller
SE531139C2 (en) * 2007-05-08 2009-01-07 Itt Mfg Enterprises Inc Pump unit and method
NO334954B1 (en) * 2012-11-12 2014-08-04 Agr Subsea As Centrifugal pump impeller and its use in pumping drilling fluid containing drill cuttings
WO2014145910A1 (en) 2013-03-15 2014-09-18 Pentair Pump Group, Inc. Cutting blade assembly
DE102014004420A1 (en) * 2014-03-27 2015-10-01 Wilo Se Centrifugal pump with cutting device
EP3449130B1 (en) 2016-04-26 2022-11-09 Pentair Flow Technologies, LLC Cutting assembly for a chopper pump
CN105971930A (en) * 2016-07-11 2016-09-28 川源(中国)机械有限公司 Centrifugal pump capable of improving flow capacity
US11786091B2 (en) * 2021-04-09 2023-10-17 Dennis M. Delany Vacuum grinder cleaning device and method

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US111026A (en) * 1871-01-17 Irvif
US1448174A (en) * 1918-03-15 1923-03-13 American Manganese Steel Co Centrifugal pump for dredging and conveying solids
FR594899A (en) * 1924-03-22 1925-09-22 G Et Weir Ltd Improvements to pump turbines
US3692422A (en) * 1971-01-18 1972-09-19 Pierre Mengin Ets Shearing pump
FI49345C (en) * 1972-05-15 1975-05-12 Ahlstroem Oy Device for preventing clogging of the sealing gap, especially in a sewage pump or the like.
JPS4962504U (en) * 1972-09-11 1974-06-01
DE2452548A1 (en) * 1973-11-19 1975-05-22 Sneek Landustrie CENTRIFUGAL PUMP
US3936758A (en) * 1973-12-03 1976-02-03 Exxon Production Research Company Phase difference detector
JPS5113403A (en) * 1974-07-23 1976-02-02 Toyo Denki Kogyosho Co Ltd SUICHUHONPUYOKATSUTAAFUAN
GB1551918A (en) * 1977-02-09 1979-09-05 Chittenden J B Pump and macerator and pump assembly
JPS5838396A (en) * 1981-08-29 1983-03-05 Ebara Corp Grinder pump
SE444969B (en) * 1982-10-11 1986-05-20 Flygt Ab Centrifugal pump intended for pumping of liquids containing solid particles
JPS6140795U (en) * 1984-08-17 1986-03-14 ソニー株式会社 Electronic device lids
JPS63188U (en) * 1986-06-17 1988-01-05

Also Published As

Publication number Publication date
FI101824B1 (en) 1998-08-31
NO900981D0 (en) 1990-03-01
NO900981L (en) 1990-10-29
DK0395604T3 (en) 1994-01-31
SE8901534D0 (en) 1989-04-27
AU622763B2 (en) 1992-04-16
NO172308B (en) 1993-03-22
CA2015572A1 (en) 1990-10-27
JPH02286898A (en) 1990-11-27
CA2015572C (en) 1995-09-05
SE466766B (en) 1992-03-30
NO172308C (en) 1993-06-30
AU4936790A (en) 1990-11-01
DE69005351T2 (en) 1994-04-14
US5011370A (en) 1991-04-30
FI101824B (en) 1998-08-31
FI900736A0 (en) 1990-02-14
DE69005351D1 (en) 1994-02-03
SE8901534L (en) 1990-10-28
JPH07111191B2 (en) 1995-11-29
ATE99025T1 (en) 1994-01-15
EP0395604A1 (en) 1990-10-31

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